Which one applies is settled before any thermal calculation: whether the contents can be pumped at all, whether the vessel already exists, and what the jacket side has to be rated for. An existing tank that must not be cut into points one way; a vessel still on the drawing board points another.
Whether the contents can be pumped, whether the vessel already exists, the design pressure and temperature of the medium, and whether the surface can be inside the tank or has to stay outside it. Corrosive contents and product contact both push toward specific answers.
Inflated panels can be formed to shape, welded into a component, hung inside a vessel or bolted to the outside of one. They are fully welded with no gaskets, they need less circulating medium than traditional dimple jacketing, and a clamp-on retrofit never cuts the pressure boundary of a tank you already own.
A tank that needs heating or cooling it does not have usually presents two expensive options: replace it, or...
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Some fluids cannot be pumped out to an exchanger. They are too viscous, too abrasive, too valuable, or the...
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Reaction heat has to leave at the rate it is produced, and the consequence of it not leaving is rarely just a...
+ Learn MoreYes, with a clamp-on Temp-Plate jacket. Panels bolt to lugs welded to the outside of the shell with heat transfer mastic between, so the pressure boundary is never cut and downtime is minimal.
Inside gives better heat transfer because the surface contacts the fluid directly. Outside avoids product contact entirely and can be retrofitted. Corrosive or abrasive contents and sanitary requirements usually decide it.
A coil contacts the fluid only along the tube. Temp-Plate gives continuous surface across the panel face, needs less circulating medium and is easier to clean around. Coils still win at very high media pressure.
Substantially less than traditional dimple jacketing, because the inflated passage volume is smaller. That shows up directly in pump size and pumping cost over the life of the system.